(19)
(11) EP 0 055 920 A3

(12) EUROPEAN PATENT APPLICATION

(88) Date of publication A3:
22.09.1982 Bulletin 1982/38

(43) Date of publication A2:
14.07.1982 Bulletin 1982/28

(21) Application number: 81306095

(22) Date of filing: 23.12.1981
(84) Designated Contracting States:
BE CH DE FR GB IT LI LU NL SE

(30) Priority: 02.01.1981 US 222196

(71) Applicant: The Standard Oil Company
 ()

(72) Inventors:
  • Presson, Robert Dean
     ()
  • Wu, Hsin-Chih
     ()
  • Sockell, Edward J.
     ()

   


(54) Process for the continuous recovery of acetonitrile


(57) A continuous process for recovering highly pure acetonitrile from crude acetonitrile containing acetonitrile, water, HCN and heavy organics, said process comprising:

(1) distilling said crude acetonitrile in a first distillation zone at a first pressure at or above 1 atmosphere to remove HCN therefrom and produce a first acetonitrile/water azeotrope and a first bottoms product containing water,

(2) distilling said first azeotrope in a second distillation zone at a second pressure less than 1 atmosphere to separate said first azeotrope into a second bottoms product containing water and a second acetonitrile/water azeotrope having a greater acetonitrile concentration than said first azeotrope, and

(3) distilling said second acetonitrile/water azeotrope in a third distillation zone at a third pressure above 1 atmosphere to produce a third acetonitrile/water azeotrope containing substantially all of the water in said second azeotrope, third bottoms product comprising acetonitrile and heavy organics and a sidestream comprising said highly pure acetonitrile.


This process enables one to obtain acetonitrile in 99+% purity. It is based upon a continuous distillation process carried out in three stages at three different pressures.





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